化学
非随机双液模型
离子液体
丁醇
四氟硼酸盐
优等
庚烷
萃取(化学)
色谱法
三元运算
溶剂
有机化学
无机化学
活度系数
乙醇
水溶液
催化作用
计算机科学
程序设计语言
作者
Gui‐Lin Wen,Xia Zhang,Xueli Geng,Yixin Ma,Jun Gao,Yinglong Wang,Zhaoyou Zhu
标识
DOI:10.1021/acs.jced.7b00635
摘要
Selection of a suitable solvent is the key for the extraction process. In this work, four ionic liquids were selected as solvent for extracting butanol, the ternary liquid–liquid equilibria (LLE) data for systems of heptane + butanol + {[HMIM][BF4] (1-hexyl-3-methylimidazolium tetrafluoroborate), [OMIM][BF4] (1-octyl-3-methylimidazolium tetrafluoroborate), [HMIM][OTf] (1-hexyl-3-methylimidazolium trifluoromethansulfonate), and [HMIM][NTf2] (1-hexyl-3-methylimidazolium bis((trifluoromethyl)sulfonyl)imide)} were measured at 298.15 K and atmospheric pressure. The extraction capacity of four ILs in the separation of butanol from heptane + butanol mixture was estimated by the selectivity (S) and solute distribution ratio (β), and the influence of the structure and anion of IL on the extraction efficiency was investigated. The experimental LLE data were correlated by using NRTL and UNIQUAC models.
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